EP2255025B1 - Procédé d enduction de surfaces métalliques avec un agent de passivation - Google Patents

Procédé d enduction de surfaces métalliques avec un agent de passivation Download PDF

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Publication number
EP2255025B1
EP2255025B1 EP09719612.5A EP09719612A EP2255025B1 EP 2255025 B1 EP2255025 B1 EP 2255025B1 EP 09719612 A EP09719612 A EP 09719612A EP 2255025 B1 EP2255025 B1 EP 2255025B1
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range
content
composition
zinc
process according
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German (de)
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EP2255025B2 (fr
EP2255025A1 (fr
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Mark Andre Dr. Schneider
Petra Grünberg
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Chemetall GmbH
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Chemetall GmbH
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
    • C23C22/362—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing also zinc cations
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08—Orthophosphates
    • C23C22/12—Orthophosphates containing zinc cations
    • C23C22/17—Orthophosphates containing zinc cations containing also organic acids
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
    • C23C22/361—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing titanium, zirconium or hafnium compounds
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
    • C23C22/364—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing also manganese cations
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C2222/00—Aspects relating to chemical surface treatment of metallic material by reaction of the surface with a reactive medium
    • C23C2222/10—Use of solutions containing trivalent chromium but free of hexavalent chromium
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C2222/00—Aspects relating to chemical surface treatment of metallic material by reaction of the surface with a reactive medium
    • C23C2222/20—Use of solutions containing silanes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/12—All metal or with adjacent metals
    • Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/1266—O, S, or organic compound in metal component
    • Y10T428/12667—Oxide of transition metal or Al

Definitions

  • the invention relates to a process for the coating of metallic surfaces with an aqueous composition which differs from phosphating solutions, the aqueous composition and the use of the process according to the invention.
  • Phosphate coatings are used on a large scale as corrosion protection layers, as a forming aid and as a primer for paints and other coatings. Especially if it is used as protection for a limited time, in particular storage and then, for example. are painted, they are referred to as a pretreatment layer before painting. However, if the phosphate coating is not followed by a lacquer coating and organic coating, treatment or passivation rather than pretreatment is used. These coatings are also referred to as conversion layers if at least one cation of the metallic surface, ie the surface of the metal part, is dissolved out and used for layer construction.
  • a phosphate coating is applied by wetting with a phosphating solution usually directly after galvanizing, but optionally also after suitable cleaning or degreasing and after rinsing with water or an aqueous medium and optionally after activation of the metallic surface and dried. Rinsing after drying of the phosphate coating could adversely affect this, especially if the phosphate coating is not or only partially crystalline.
  • the high-grade phosphating solutions and phosphate coatings contain a significant amount of zinc, manganese and nickel.
  • nickel is to be avoided because of its toxicity and harmfulness.
  • the unavoidable heavy metal contents in the waste water, in the phosphate sludge and in the grinding dust are disturbing.
  • DE 102006052919 A1 teaches aqueous compositions for anticorrosive conversion treatment of metallic surfaces based on 5-50 g / L phosphate, 0.3-3 g / L zinc and 0.001-0.2 g / L titanium or / and zirconium in water-soluble titanium / zirconium -Links.
  • a titanium or / and zirconium compound is used in a phosphating solution in a phosphating process, the contents of these compounds are typically less than 0.2 g / L in total. Because it is known that higher contents of these compounds usually lead to coating defects especially on aluminum-rich surfaces. Very rarely, a complexing agent is added to a phosphating solution. If in very rare cases a silane is used in a phosphating solution in a phosphating process, the contents are very low. But a combination of these additives is never used in phosphating.
  • WO 96/07772 A1 describes acidic aqueous liquid compositions based on anions of fluoride complexes, di- or tetravalent cations of Co / Mg / Mn / Zn / Ni / Sn / Cu / Zr / Fe / Sr, phosphonate and organic polymer.
  • EP 1 205 580 A1 relates to chemically treated steel sheets having a zinc-containing layer and a conversion coating of a water-soluble complex manganese compound or a water-insoluble complex titanium compound and at least one organic acid, wherein the conversion coating is dried without rinsing and wherein the composition for the conversion coating manganese, titanium, phosphoric acid or phosphate, fluoride and at least one organic acid and / or its salt and has a pH in the range of 1 to 6.
  • WO 02/24975 A1 discloses aqueous acidic liquid compositions based on anions of fluoride complexes di- or tetravalent cations of Co / Mg / Mn / Zn / Ni / Sn / Cu / Zr / Fe / Sr, phosphate, phosphonate and organic polymer.
  • DE 102005015573 A1 discloses a method of coating metallic surfaces with a silane / silanol / siloxane / polysiloxane containing aqueous composition having Ti / Hf / Zr / Al / B containing compound contents and cations and at least one other compound.
  • WO 2004/053183 A2 refers to aqueous liquid compositions based on complex fluorine-containing acids, water-soluble organic carboxylic acids, phosphate, tannin and polymeric aminophenol compound.
  • the method according to the invention is a conversion coating method of the first type.
  • the coil (reel) is usually to be processed by the steel manufacturer in further processing operation without rust approaches.
  • good formability or / and also good alkali resistance in mild alkaline cleaning and / or during forming with alkaline emulsions is / are advantageous for some embodiments.
  • the coating should also possible after forming have a good corrosion protection and preferably also a good paint adhesion.
  • the aqueous composition according to the invention will be a solution unless particles or / and an emulsion are added, as long as this solution is stable and does not tend to precipitate.
  • additive or “adding” in the context of this application means that at least one such substance or mixture is added.
  • composition according to the invention and the method according to the invention are used in particular for passivating the metallic surface, but can also be used for pretreatment before a subsequent coating, for example with an organic coating and for other purposes be used.
  • passivation is understood to mean the coating of metallic surfaces in which no subsequent organic coating is normally applied for permanent protection against corrosion. However, in some cases passivation does not preclude the subsequent application of at least one organic coating such as a primer or even a paint system and / or an adhesive.
  • the aqueous composition according to the invention preferably contains cations of aluminum, chromium (III), iron, manganese or / and zinc or / and at least one compound containing aluminum, chromium (III), iron, manganese or / and zinc.
  • the starting composition according to the invention that is to say in particular the fresh concentrate and / or the fresh bath composition, but often also the supplementary solution which is added to the bath in use as needed, in particular in order to obtain the bath ready for use, preferably contains a substantial content in many embodiments on cations and / or on at least one compound of aluminum, chromium (III), iron, manganese or / and zinc.
  • the composition in addition to the cations and / or compounds of aluminum, chromium, iron, manganese, titanium, zinc and / or zirconium, it contains no or no substantial content of other heavy metal cations and / or heavy metal compounds in addition to those just mentioned. Often, it also contains no chromium content. However, in contact with the equipment, with the metallic surfaces to be coated or / and by entrainment of impurities, the composition may often take up further cations and / or compounds. Therefore, the original chromium-free composition may also contain traces or occasionally even low contents, for example of chromium and / or chorn compounds or / and cations / compounds from other steel refiners.
  • the composition preferably contains a total content of cations of aluminum, chromium (III), iron, manganese or / and zinc or / and of at least one compound containing aluminum, chromium (III), iron, manganese or / and zinc in the range from 3.5 to 100 g / L calculated as Metail.
  • the composition preferably contains a total content of cations of aluminum, chromium (III) or / and zinc or / and of at least one compound containing aluminum, chromium (III) or / and zinc in the range from 3.5 to 100 g / L calculated as metal.
  • the contents of aluminum, chromium (III), iron, manganese or / and zinc or of aluminum, chromium (III) or / and zinc in the range from 3.5 to 90, from 3.5 to 80 are very particularly preferred. from 3.5 to 70, from 3.5 to 60, from 3.5 to 50, from 4 to 40, from 4.5 to 35, from 5 to 30, from 5.5 to 25, from 6 to 20 or from 8 to 14 g / L, calculated as metal. Particularly preferred is a content of chromium (III) as cations and / or compounds NuII, in about NuII or in the range of 0.01 to 30, from 0.1 to 20, from 0.3 to 12, from 0.5 to 8, from 0.8 to 6 or from 1 to 3 g / L calculated as metal.
  • composition according to the invention with respect to the cations and / or the metal-containing compounds consists only of cations of aluminum, chromium (III) or / and zinc or / and of at least one compound containing aluminum, chromium (III) or / and Zinc.
  • the content of chromium (VI) as cations and / or compounds may be in particular zero, about zero or in the range of 0.01 to 8, from 0.05 to 5, from 0.1 to 3 or from 0.3 to 1 g / L calculated as metal.
  • at least 60%, at least 80%, at least 90% or even at least 95% of these cations and compounds are those based on aluminum and / or zinc.
  • the content of such cations and compounds can be varied widely.
  • the composition according to the invention contains essentially only cations of aluminum, titanium, zinc or / and zirconium or only these are added to the composition. It is particularly preferred that only cations and / or compounds of aluminum, chromium (III), titanium, zinc or / and zirconium are added to the composition according to the invention with respect to the cations and / or metal-containing compounds.
  • the composition according to the invention contains only or essentially only titanium and zinc or titanium and aluminum or are added to the composition. It is particularly preferred that the composition of the invention with respect to the cations and / or Metal containing compounds only cations and / or compounds of aluminum, chromium (III), titanium, zinc or / and zirconium are added.
  • further types of cations in particular trace impurities, introduced impurities or / and impurities thrown out of devices or / and substrates, may occur.
  • the content of cations and / or at least one compound of alkaline earth metals is about zero or in the range of 0.001 to 1.5 g / L, from 0.003 to 1 g / L, of 0.01 to 0.5 g / L or from 0.03 to 0.1 g / L, calculated as the respective metal. If the content of these cations / compounds is very low, no disadvantages are to be expected. If the content of these cations / compounds is too high, the stability of the solution is endangered and losses in corrosion protection are to be expected. Alkaline earth metal levels usually interfere with precipitation. Due to the levels of fluoride (including complex fluoride) alkaline earth metal precipitation can easily occur.
  • the content of cations and / or at least one compound of at least one alkali metal is about zero or in the range of 0.001 to 1.5, from 0.01 to 1, from 0.1 to 0.5, of 0.02 to 0.15 g / L, calculated as the respective metal.
  • low alkali metal contents and alkaline earth metal contents often do not interfere when they are on the order of the levels of city water.
  • the aqueous composition of the present invention preferably has a content of phosphate in the range of 6 to 400 g / L calculated as PO 4 . More preferably, the phosphate content of the composition ranges from 6 to 350, from 12 to 300, from 18 to 280, from 25 to 260, from 30 to 240, from 40 to 220, from 50 to 200, from 60 to 180, of 70 to 160, from 85 to 140 or from 100 to 120 g / L. If the content of phosphate is too low, the corrosion protection is low.
  • a phosphate additive is so high that a significant improvement in corrosion protection and the surface appearance. If the phosphate content is too high, dull coatings may form.
  • the ratio of Al: PO 4 in the case of compositions whose content of cations and / or inorganic compounds selected from those based on aluminum, chromium, iron, manganese or / and zinc predominantly comprises those based on aluminum is in the range of 1 : 10 to 1: 25, in particular in the range of 1: 12 to 1: 18.
  • the ratio of Zn: PO 4 in compositions whose content of cations and / or inorganic compounds selected from those based on aluminum, chromium, Iron, manganese and / or zinc or based on aluminum, chromium and / or zinc predominantly those based on zinc in the range of 1: 4 to 1: 20, in particular in the range of 1: 6 to 1: 15.
  • a phosphate additive may be a monometal phosphate additive, an additive of phosphoric acid and metal, phosphoric acid and metal salt / metal oxide, diphosphate, triphosphate, polyphosphate or / and phosphorus pentoxide to water or to an aqueous mixture.
  • At least one orthophosphate is added to the aqueous composition with an overall addition of Range of 1 to 400 g / L calculated as PO 4 , more preferably in the range of 5 to 300, from 10 to 250, from 15 to 200, from 20 to 150, from 25 to 100, from 30 to 80 or from 40 to 60 g / L.
  • the total addition corresponds to the total salary.
  • the aqueous composition can be prepared with phosphoric anhydride P 2 O 5 , with a phosphorus-containing acid, with at least one salt or / and esters of orthophosphoric acid and / or with at least one salt or / and esters of a condensed phosphoric acid, optionally together with at least one Metal, carbonate, oxide, hydroxide or / and salt such as nitrate together with phosphoric acid.
  • the addition of at least one complexing agent may be advantageous and / or necessary if the pH is to be increased, when diluting the composition with water, when receiving levels of ions and / or compounds, in particular of other types of ions and / or other compounds or / and to stabilize the composition, in particular to prevent precipitation and / or dissolve. It serves to increase the content of compounds, in particular of cations such as aluminum, chromium, iron, manganese, zinc and / or of cations which are introduced, of being leached out of plants or / and of being leached out of the metallic surfaces, in US Pat Keep the composition dissolved.
  • cations such as aluminum, chromium, iron, manganese, zinc and / or of cations
  • precipitations such as fluorides, oxides, hydroxides or / and phosphates in particular of aluminum, iron, manganese or / and zinc can interfere because increasingly form sludge.
  • complexing agents can be added as needed to re-dissolve the precipitate.
  • the at least one complexing agent serves in particular to complex cations such as aluminum, chromium, iron, magnesium, manganese, titanium, zinc and / or zirconium and thereby stabilize the solution or suspension, in particular at lower acidity.
  • an addition of at least one complexing agent also has more or less corrosion protection proved.
  • complexing agent in the context of this application also includes chelating agents.
  • the complexing agent used is then at least one compound based on phosphonic acid and / or on the basis of phytic acid and / or on the basis of tannic acid.
  • the content of complexing agent (s) can be varied within wide ranges.
  • the aqueous composition according to the invention contains a total content of at least one complexing agent in the range from 1 to 200 g / l.
  • the total content of at least one complexing agent is more preferably in the range from 2 to 180, from 3 to 160, from 4 to 130, from 5 to 100, from 6 to 80, from 8 to 70, from 10 to 60, from 12 to 50 , from 15 to 40 or from 20 to 30 g / L.
  • the complexing agent content is so high that the composition is a stable solution and that optionally stable solutions are obtained even when diluted with water.
  • the aqueous composition may preferably contain at least one phosphonic acid, at least one salt of a phosphonic acid and / or at least one ester of a phosphonic acid be added.
  • the aqueous composition contains at least one phosphonic acid based compound in the range of from 1 to 200 g / L, more preferably in the range of from 0.3 to 150, from 1 to 80, from 1.5 to 50 or from 2 up to 30 g / L.
  • At least one compound based on phosphonic acid for example diphosphonic acid, diphosphonic acid with an alkyl chain, for example 1-hydroxyethane-1,1-diphosphonic acid (HEDP), aminotris (methylenephosphonic acid) (ATMP), ethylenediaminetetra (methylenephosphonic acid) (EDTMP) , Diethylenetriamine-penta (methylenephosphonic acid) (DTPMP), diethylenetriaminepenta (methylenephosphonic acid) (DTPMP), hexamethylenediamine-tetra) methylenephosphonic acid) (HDTMP), hydroxyethylamino-di (methylenephosphonic acid) (HEMPA) or / and phosphonobutane-1,2,4 tricarboxylic acid (PBTC).
  • HEDP 1-hydroxyethane-1,1-diphosphonic acid
  • ATMP aminotris
  • ETMP ethylenediaminetetra
  • DTPMP diethylenetriamine-penta (methylenephospho
  • the composition according to the invention contains at least one compound based on phytin or / and tannin.
  • compounds such as phytic acid, tannic acid and / or their derivatives such as their salts and their esters including their modified compounds and their derivatives.
  • Compounds based on this chemical base can often have a positive influence on corrosion protection in a special way. They also act as complexing agents and are counted for the purposes of this application to the complexing agents.
  • the composition in particular of the compounds based on tannin can vary considerably - for example, depending on the natural raw materials used - and their optionally carried out cleaning and / or chemical modification. They are partly colored.
  • the aqueous composition contains at least one compound based on phytin or / and tannin with a total content of these compounds in the range from 0.05 to 30 g / L, particularly preferably in the range from 0.3 to 25 g / L or from 1 to 20 g / L, most preferably in the range of 1.5 to 15 g / L or from 2 to 10 g / L.
  • the aqueous composition preferably contains a total content of at least one titanium or / and zirconium compound of at least 5 g / L, 10 g / L, 15 g / L, 20 g / L or 25 g / L.
  • this total content is in the range of 3 to 200 g / L. It is often present in a content in the range of 3 to 100 g / L of Ti or / and Zr calculated as metal. It may optionally be added partially or wholly as at least one complex fluoride and / or partially or wholly present as at least one complex fluoride in the aqueous composition.
  • the aqueous composition contains a total content of at least one titanium or / and zirconium compound in the range of from 3 to 160, from 3 to 130, from 4 to 100, from 5 to 80, from 6 to 60, from 8 to 50, of 10 to 40 from 15 to 30 or from 20 to 25 g / L. More preferably, the content of Ti or / and Zr calculated as the metal in the aqueous composition is in the range of from 3 to 90, from 6 to 80, from 10 to 70, from 20 to 60, or from 35 to 50 g / L.
  • at least one complexing agent such as a phosphonate and / or at least one protective compound such as a surfactant
  • the fluoride-containing compound only at least one titanium or / and zirconium compound based on complex fluoride is added.
  • the composition contains at least one complex fluoride and / or its salt of aluminum, titanium, zinc or / and zirconium, which are present approximately as MeF 4 or / and MeF 6 complex.
  • the aqueous composition contains at least one complex fluoride based titanium and / or zirconium compound in the range of from 1 to 200, from 1.5 to 175, from 2 to 150, from 3 to 120, from 4 to 100, from 5 to 80, from 6 to 60, from 8 to 50, from 10 to 40 from 15 to 30 or from 20 to 25 g / L.
  • the addition and content of at least one titanium or / and zirconium compound is so high that a good bare corrosion protection and, if necessary, a good paint adhesion to the subsequent paint / primer coating occurs.
  • the content of at least one titanium and / or zirconium compound is too high and if complexing agents are present in an insufficient amount, instability of the bath and hence precipitation can easily occur. Because a fluoride or a complex fluoride can also act as a complexing agent. However, fluoride and complex fluoride are not counted as complexing agents for the purposes of this application.
  • the addition and content of a titanium compound has proved to be particularly advantageous for improving the corrosion protection.
  • the addition and content of a zirconium compound has proved to be advantageous in particular in hot-dip galvanized surfaces for improving the paint adhesion.
  • the titanium or / and zirconium compound according to the invention may be at least one corresponding complex fluoride and / or at least one complexed substance such as at least one titanium chelate, in particular at least one titanium alkoxide, the less reactive titanium and / or zirconium compounds being preferred.
  • the composition of the invention contains at least one titanium or / and zirconium-containing fluoride-free compound, such as a chelate.
  • This compound can serve to incorporate titanium or / and zirconium into the composition in a different form and is therefore a possibility of a source of such a compound.
  • Such a compound can significantly improve the corrosion protection and stably keep the aqueous composition in solution.
  • the composition of the invention contains a content of titanium and / or zirconium chelates in the range of 0.1 to 200 g / L, more preferably in the range of 1 to 150, 3 to 110, 5 to 90, 7 to 70, 10 to 50 or 15 to 30 g / L.
  • the content of such compounds is selected such that a content of titanium or / and zirconium in the range from 3 to 60 or 5 to 45 mg / m 2 remains on the metallic surface, calculated as metal, determined by X-ray fluorescence.
  • a compound is added in particular if no other titanium- or / and zirconium-containing compound is present in the composition according to the invention. Because it is particularly advantageous that at least one titanium or / and zirconium-containing compound is contained in the composition according to the invention.
  • dihydroxo bis (ammonium lactate) titanate can be used as such a compound.
  • the aqueous composition contains preferably approximately no fluoride content or a content of free fluoride F free in the range of 0.01 to 5 g / l and / or a content of total fluoride F tot in the range of 3 to 200 g / L.
  • the composition contains a content of free fluoride F free in the range of 0.1 to 3.5, 0.3 to 2 or from 0.5 to 1 g / L or / and a content of Total fluoride F total in the range of 3 to 180, from 5 to 140, from 8 to 110, from 10 to 90, from 12 to 75, from 15 to 60 or from 20 to 40 g / L.
  • no hydrofluoric acid, no monofluoride or / and no bifluoride is added to the composition of the invention.
  • a content of hydrofluoric acid, monofluoride or / and bifluoride in the composition according to the invention can be formed in small amounts from at least one complex fluoride or / and its derivative only on the basis of the equilibrium conditions.
  • the inventive composition hydrofluoric acid, monofluoride and / or bifluoride is calculated with a total content of 0.01 to 8 g / L as free fluoride F free , in particular from 0.1 to 5 or from 0.5 to 3 g / L. added.
  • silane should also include their hydrolysis, condensation, polymerization and reaction products, ie in particular silanols, siloxanes and optionally polysiloxanes.
  • polysiloxane is intended to include the condensation, polymerization and reaction products of the polysiloxane.
  • the composition in individual embodiments contains no content of at least one silane / silanol / siloxane / polysiloxane and in many embodiments preferably a content of at least one silane / silanol / siloxane / polysiloxane in the range from 0.1 to 200 g / L , calculated on the basis of silane or polysiloxane of the respective starting compound.
  • At least one surfactant wetting agent
  • a content of at least one surfactant can in some cases have a very strong influence on the properties of the coating according to the invention, in particular in corrosion protection.
  • the corrosion protection can be significantly improved in particular with less high quality grades of HDG.
  • at least one nonionic surfactant is added, optionally alternatively or additionally, at least one cationic surfactant.
  • a second surfactant may optionally act as a solubilizer. especially added as silane / silanol / siloxane or / and as polysiloxane, the corrosion protection often improves significantly.
  • at least one silane is added while at least one polysiloxane is added only in individual embodiments either alone or in addition to at least one silane.
  • the composition preferably contains in each case at least one silane / silanol / siloxane / polysiloxane, in particular based on alkoxysilane, alkylsilane, amidosilane, aminosilane, bis-silyl-silane, epoxysilane, fluorosilane, imidosilane, iminosilane, isocyanatosilane, (meth) acrylatosilane or / and vinyl silane.
  • silanes / silanols / siloxanes / polysiloxanes aminosilanes-based silanes / silanols / polysiloxanes have been found to be particularly useful, although the other silanes / silanols / siloxanes referred to herein may also be important depending on the embodiment.
  • a content of silanes / silanols / siloxanes having at least one nitrogen-containing group such as, in each case, at least one amino group ( aminosilanes), amido group, imino group or / and imido group.
  • the alkylsilanes may in particular be di-, tri- and / or tetrafunctional.
  • the alkyl silanes may in particular be without an organically functional side chain or, in particular, may have a terminal nitrogen-containing group.
  • the alkylsilanes may optionally be without side chain, but may also have at least one side chain with a chain length of up to ten carbon atoms.
  • the aqueous composition comprises each an addition of and content of at least one compound based on at least one silane / silanol / siloxane / polysiloxane a) having at least one nitrogen-containing group such as at least one amino group or ammonium group, b) based on of bis-silane (s), c) based on epoxysilane (s), d) based on fluorosilane (s), e) based on isocyanatosilane (s), f) based on (meth) acrylatosilane (s) , g) based on vinylsilane (s), h) based on alkoxysilanes and / or i) based on alkylsilane, in each case in the range from 0.5 to 160 g / l, particularly preferably in the range from 1 to 120, of 2 to 80, from 3 to 50, from 5 to 35 or from 8 to 20 g /
  • silanes are 3-aminopropyltriethoxysilane and / or 3-aminopropyltrimethoxysilane (APS), N- [2- (aminoethyl)] - 3-aminopropyltrimethoxysilane (AEAPS), methylsilane, butylsilane, epoxysilane or / and tetraethoxysilane (TEOS).
  • APS 3-aminopropyltriethoxysilane and / or 3-aminopropyltrimethoxysilane
  • AEAPS N- [2- (aminoethyl)] - 3-aminopropyltrimethoxysilane
  • methylsilane butylsilane
  • epoxysilane or / and tetraethoxysilane TEOS
  • HF gas may form at higher fluoride levels.
  • siloxanes and / or polysiloxanes it is also possible to form siloxanes and / or polysiloxanes.
  • addition of and content of at least a polysiloxane or the addition of a combination based on silane and polysiloxane may be advantageous.
  • the composition preferably contains at least one organic monomer / oligomer / polymer / copolymer.
  • copolymer in the sense of this application also includes block copolymers and / or graft copolymers.
  • the addition of and content of at least one such organic compound, preferably at least in part based on (meth) acrylic, epoxy, ethylene, polyester or / and urethane, is important in some embodiments to provide corrosion protection, paint adhesion, formability, etc.
  • the latter is often used to avoid the cleaning of oiled and / or soiled metallic surfaces.
  • the aqueous composition contains at least one organic monomer / oligomer / polymer / copolymer content in the range of from 0.1 to 180 g / L, more preferably in the range of from 2 to 120, from 5 to 80, from 8 to 55, or from 12 to 30 g / L.
  • the content of organic monomer / oligomer / polymer / copolymer is so high that the formability is improved, in particular, the friction during forming is reduced.
  • the content of organic monomer / oligomer / polymer / copolymer is so low that the stability of the aqueous composition is maintained and a good surface appearance of the coating is ensured, so that in particular no dull or / and streaky coatings arise.
  • the composition contains at least one organic monomer / oligomer / polymer / copolymer based on or / and containing (meth) acrylic, epoxy, ethylene, polyester or / and urethane.
  • the at least one ingredient mentioned herein may also be at least one component of copolymer (s).
  • the aqueous composition preferably comprises a content of at least one organic monomer / oligomer / polymer / copolymer based on a) (meth) acryl, b) epoxide, c) ethylene, d) polyester or / and e) urethane in each case in the range from 0 , 5 to 80 g / L, more preferably in the range of 2 to 60, from 5 to 50, from 8 to 40 or from 15 to 30 g / L.
  • the composition preferably contains in each case at least one inorganic or / and organic compound in particle form.
  • organic particles may be present as a component of organic polymer / copolymer.
  • the aqueous composition contains a content of inorganic and / or organic particles in the range of 0.05 to 80 g / L, more preferably in the range of 0.3 to 50, from 1 to 30, from 1.5 to 15 or from 2 to 10 g / L.
  • the composition according to the invention preferably contains at least one inorganic compound in particle form based on Al 2 O 3 , SiO 2 , TiO 2 , ZnO, ZrO 2 or / and corrosion protection particles which have a mean particle diameter of less than 300 nm measured under a scanning electron microscope.
  • the inorganic particles such as those based on Al 2 O 3 , SiO 2 , TiO 2 or / and ZrO 2 often act as particles with barrier effect and optionally with connection to the metallic surface.
  • ZnO particles for example, can have a corrosion-protecting effect up to their possibly occurring dissolution.
  • the corrosion protection particles may in particular be those based on, for example, silicate, especially alkali silicate and / or alkaline earth silicate, but also based on phosphates, phosphosilicates, molybdates, etc. Corrosion protection particles can in particular due to their barrier function and / or the release of ions, they help to protect against corrosion.
  • the content of inorganic particles is so low that no disturbing friction during forming occurs.
  • the content of inorganic particles is so high that the particles exert a barrier function and increased corrosion protection is achieved.
  • the composition according to the invention contains at least one accelerator, e.g. at least one accelerator selected from the group consisting of accelerators based on chlorate, nitrite, nitrobenzenesulfonate, nitroguanidine, perborate and at least one other nitroorganic compound with oxidizing properties which are known from phosphating. These compounds can also help to reduce or eliminate the formation of hydrogen gas at the interface with the metallic surface.
  • the aqueous composition contains at least one of these accelerators in the range of 0.05 to 30 g / L, more preferably in the range of 0.3 to 20, from 1 to 12, from 1.5 to 8 or from 2 to 5 g / L.
  • the composition according to the invention preferably comprises at least one additive such as in each case at least one wetting agent, a demulsifier, an emulsifier, a defoamer, a corrosion inhibitor and / or a wax. If necessary, at least one additive can be added, as is customary and basically known in the case of conversion coatings, passivations or lacquers / primers.
  • the aqueous composition contains at least one additive having a total content of the additives in the range from 0.001 to 50 g / L, more preferably in the range from 0.01 to 30, from 0.1 to 10, from 0.5 to 6 or from 1 up to 3 g / L.
  • the object is further achieved with a coating produced by the method according to the invention on a metallic surface.
  • the weight ratio of (Al, Cr 3+ , Fe, Mn and Zn) is: (Ti and Zr) or / and of (Al, Cr 3+ and To): (Ti and Zr) in the range of 0.1: 1 to 3: 1. Particularly preferred are these weight ratios in the range of 0.5: 1 to 2.5: 1 or from 1: 1 to 2: 1.
  • these and optionally also other cations may be present in the composition according to the invention: on the one hand by entrainment e.g. from previous baths, by impurities or / and by dissolving e.g. from tank and pipe materials as well as from the surfaces to be coated, on the other hand by adding further cations / compounds with a metal content such as e.g. at least one alkali metal, molybdenum or / and vanadium.
  • a metal content such as e.g. at least one alkali metal, molybdenum or / and vanadium.
  • the aqueous composition of the present invention is free or substantially free of compounds based on carboxylic acid, acrylic acid, phenol, starch, chromium (VI) or / and based on other heavy metals, e.g. those based on chromium, molybdenum, nickel, vanadium or / and tungsten.
  • the aqueous composition according to the invention is preferably free or substantially free of compounds which are used as accelerators in the phosphating, in particular of compounds based on chlorate, nitrite, nitroguanidine, peroxide or / and other N-containing accelerators.
  • compositions of the invention are preferably free or substantially free of chromium (VI). However, they may also be free or substantially free of chromium (III), in some cases optionally free or substantially free of cations and / or compounds of chromium, in some of the compositions according to the invention.
  • the aqueous composition contains no or only a content of calcium and / or magnesium of not more than 0.5 g / L, more preferably not more than 0.15 g / L, or / and at least one toxic or environmentally unfriendly heavy metal such as chromium of not more than 0.5 g / L, more preferably not more than 0.15 g / L.
  • Fluoride-free compositions may also contain some or more calcium or / and magnesium.
  • the composition according to the invention preferably has a pH in the range from 0 to 10.
  • the pH is in the range from 0.3 to 8, from 0.5 to 6, from 0.8 to 5, from 1 to 4 or from 2 to 3.
  • Concentrates often have a pH value in the range of 0 , 3 to 3, baths often from 1.5 to 4.
  • the pH is often at the beginning of the work, at high concentrations or / and in non-truncated systems at values of 0.1 to 2, often in the range of 0 , 3 to 1.
  • the pH in a range from 1 to 10, in particular from 1.5 to 7, from 1.8 to 5 or from 2 to 3.5 are raised, which is often advantageous.
  • the at least one amine compound or / and at least one polyamine compound is in many cases also suitable as a pickling inhibitor.
  • a pH of the composition in the range from 2 to about 10 can be set, in which case an increased amount of at least one approximately neutral or / and basic compound is added.
  • at least one other basic and optionally nitrogen-containing compound, at least one basic carbonate, hydroxide or / and oxide-containing compound, at least one organic polymer / copolymer or / and at least one silane / silanol / Siloxane / polysiloxane are added.
  • zinc oxide, manganese carbonate or / and substantially neutral or basic polymers or / and copolymers are added.
  • the content of approximately neutral or / and basic agents which help to adjust the pH and added predominantly or only for the purpose of pH adjustment may preferably be zero or in the range of 0.05 to 100 g / L , more preferably in the range of 0.2 to 60, from 1 to 40, from 2 to 25, from 3 to 18 or from 4 to 12 g / L. Due to levels of fluoride or / and silane / polysiloxane, it may be advantageous not to measure with a glass electrode but to use pH indicator paper.
  • the aqueous composition preferably has values of the free acid FS (FA) in the range of 2 to 25 points, values of the total acid GS (TA) in the range of 20 to 45 points or / and values of the total acid Fischer GSF (TAF) in the range of 12 to 20 points.
  • the acid value S for the ratio of FS: GS (FA: TA) is preferably in the range of 0.1 to 0.6.
  • the acid value S for the ratio of FS: GSF (FA: TAF) is preferably in the range of 0.2 to 1.3.
  • the values of the free acid FS are in the range of 6 to 16 points, values of the total acid GS (TA) in the range of 27 to 37 points or / and values of the total acid Fischer GSF (TAF) in the range of 15 to 18 points. More preferably, the acid value S for the ratio of FS: GS (FA: TA) is in the range of 0.2 to 0.5 or / and the acid value S for the ratio of FS: GSF (FA: TAF) is in the range of 0 , 35 to 1.0. These values apply to titrations at concentrations of 60 g / L of solids and active substances, with the exception of ammonia levels.
  • An amount of 60 g of the aqueous composition to be analyzed is first made up to 1 liter with water and then diluted. To determine the free acid, 10 ml of the composition after dilution to 100 ml with deionized water (deionised water) using a Titroprocessor and an electrode with 0.1 M NaOH titrated to the inflection point. The consumed amount of 0.1 M NaOH per 10 ml of diluted composition gives the value of free acid (FS) in points.
  • FS free acid
  • the total content of phosphate ions is determined by titrating the titration solution to the 2nd inflection point after addition of potassium oxalate solution using a Titroprocessor and an electrode with 0.1 M NaOH following determination of the free acid.
  • the consumption of 0.1 M NaOH for 10 ml of the diluted composition corresponds to Fischer's total acid (GSF). If this value is multiplied by 0.71, the total content of phosphate ions is calculated as P 2 O 5 ( See W. Rausch: "The phosphating of metals”. Eugen G. Leuze-Verlag 1988, pp. 300 ff ).
  • the so-called S value for the ratio FS: GS or FS: GSF is obtained by dividing the value of the free acid by the value of the total acid or total acid according to Fischer.
  • the total acid is the sum of the divalent cations present as well as free and bound phosphoric acids (the latter being phosphates). It is determined by the consumption of 0.1 molar sodium hydroxide solution using a Titroprozessors and an electrode. This consumption per 10 ml of the diluted composition corresponds to the total acid score.
  • Table 2 gives an overview of measurement results. These are formulations with the same starting composition, in which only the pH was varied with different amounts of ammonia.
  • the compounds which are also contained in the solution in appropriate components are added as additives to the aqueous concentrate for the preparation of an aqueous composition.
  • the composition of the bath is preferably by Dilute the aqueous concentrate with 10 to 1000% of the solids and active ingredient content of the concentrate made with water from the aqueous concentrate. But even a highly concentrated or / and undiluted solution or dispersion can be advantageously used in some embodiments.
  • All metallic materials can be coated with their metallic surfaces .
  • metallic surfaces of aluminum, iron, copper, magnesium, titanium, zinc, tin and / or their alloys are coated, in particular zinc, steel, galvanized (hot dip galvanized, HDG), electrolytically galvanized, Galvalume ® -, Galfan ® - or / and Alusi ® surfaces.
  • the composition according to the invention has proved to be outstanding, especially with zinc-rich or / and aluminum-rich metallic surfaces.
  • For surfaces of iron and steel materials in particular compositions having a pH in the range of 4 to 10, in particular of at least 5 or even of at least 7 have been recommended in order to avoid rapid rusting (flash rusting).
  • the metallic components coated by the process according to the invention can be used in particular in vehicle construction, as architectural elements in construction or for the manufacture of devices and machines, such as, for example, domestic appliances.
  • the coating produced according to the invention may have a widely varying coating composition.
  • it may be characterized in that it contains: Al, Cr or / and Zn are calculated as metal 1 to 100 mg / m 2 , Ti or / and Zr calculated together as metal 1 to 100 mg / m 2 , Si compound (s) calculated as metal 0.1 to 25 mg / m 2 or / and P 2 O 5 3 to 400 mg / m 2 .
  • the coating according to the invention particularly preferably contains: Al, Cr or / and Zn are calculated as metal 10 to 70 mg / m 2 , Ti or / and Zr calculated together as metal 10 to 70 mg / m 2 , Si compound (s) calculated as metal 1 to 15 mg / m 2 or / and P 2 O 5 80 to 220 mg / m 2 .
  • the weight ratio of (Al, Cr 3+ and Zn): (Ti and Zr) of the coating composition may preferably be in the range of 0.5: 1 to 1.8: 1, more preferably in the range of 0.9: 1 to 1.4: 1.
  • the layer weight of the layer formed according to the invention can vary within wide limits. It may range from 0.01 to 12, from 0.05 to 10, from 0.1 to 8, from 0.3 to 6, from 0.5 to 4 or from 0.8 to 2 g / m 2 , In the case of coating in strip systems, it can be in the range from 10 to 1000 mg / m 2 , preferably in the range from 30 to 800 or from 60 to 650 mg / m 2 , more preferably in the range from 100 to 500 or from 130 to 400 mg / m 2 , very particularly preferably in the range from 160 to 300 or from 200 to 250 mg / m 2 .
  • the total content of titanium or / and zirconium in the dry film is preferably in the range of 1 to 100 mg / m 2 of Ti or / and Zr calculated as metal, particularly preferably in the range of 10 to 60 mg / m 2 .
  • the total content of titanium or / and zirconium can be measured, for example, by X-ray fluorescence.
  • the total content of silicon in the dry film when coated in strip lines is preferably in the range from 1 to 80 mg / m 2 of Si calculated as metal, more preferably in the range of 3 to 40 mg / m 2 .
  • the total content of P 2 O 5 in the dry film is preferably in the range of 30 to 400 mg / m 2 of P 2 O 5 , particularly preferably in the range of 60 to 300 mg / m 2, when coated in strip lines.
  • the thickness of the coatings according to the invention is often in the range from 0.01 to 5.0 ⁇ m, in particular in the range from 0.5 to 3.5, from 0.8 to 2.5 or from 1.0 to 2, when coating in strip systems , 0 ⁇ m.
  • the thickness of the coating is often in the range of 0.01 to 1.2 microns, in particular in the range of 0.1 to 1.0, from 0.2 to 0.8 or from 0.3 to 0.6 microns.
  • the aqueous compositions of the invention often have a concentration of solids and active ingredients (total concentration) in the range of 10 to 800 g / L.
  • a concentrate may often have a total concentration in the range of 200 to 800 g / L, especially from 400 to 750 g / L. It can be diluted with water if necessary.
  • the dilution of a concentrate is preferably carried out by a factor in the range of 1.1 to 25, more preferably in the range of 1.5 to 16, from 2 to 10 or from 3 to 6.
  • the content of solids and active ingredients in the aqueous The composition depends above all on the type of substrate to be coated, on the particular installation and on the wet film thickness caused by the installation.
  • the composition of the invention is used on metallic strip in coil coating processes.
  • Many of the belt systems have a belt speed in the range of 10 to 200 m / min. The faster the belt is driven, the faster the reactions between the composition according to the invention and the metallic surface must take place so as not to require too long plant sections.
  • the reaction time between application of the composition and its complete drying can take from a fraction of a second up to about 60 seconds. This may, in particular in the case of the faster belt systems, mean that the aqueous composition is too less reactive and therefore has to have a stronger acidity and a stronger pickling power.
  • its pH is in the range of 0.5 to 3.5 in coil coating processes.
  • the concentration of all solids and active ingredients of the aqueous composition for coating in belt plants is often in the range of 200 to 800 or from 300 to 650 g / L.
  • the contents of individual components or additives are adjusted according to the total contents.
  • the aqueous composition is applied to the clean or cleaned metallic strip applied as a wet film by spraying and squeezing, which often has a wet film thickness in the range of 1 to 4 microns.
  • a Chemcoater or Rollcoater can be used instead.
  • the wet film is dried on metallic strips or sheets ( dry or no-rinse method ).
  • the drying may preferably be carried out in a temperature range from about room temperature to about 75 ° C peak metal temperature (PMT).
  • the composition according to the invention can be aligned, for example, by means of suitable concentration and suitable pH, especially for a slow or rapid treatment in a belt system.
  • neither the wet film, nor the dried film is rinsed with water, so that the abandonedbeizten from the metallic surface cations and compounds are not removed, but are incorporated into the coating.
  • the reaction time between the first contacting of the composition until its complete drying (no-rinse process) or until rinsing off the components which can be removed by rinsing with water (rinse method) preferably take 0.5 to 10 minutes. Longer times are possible in principle.
  • the concentration of all solids and active ingredients of the aqueous composition is often in the range of 10 to 300 or 30 to 200 g / L.
  • compositions it may also happen that in contact with the composition according to the invention substantially only a staining effect and / or only a very thin coating occurs, so that, for example, in hot-dip galvanized surfaces on zinc grain boundaries the zinc crystallization image is recognizable. This also illustrates the difference to a phosphating.
  • the coating according to the invention in contrast to a phosphate layer, offers an unusually strong blank corrosion protection, even if the coating according to the invention is often much thinner than a phosphate layer and even if it is chromium-free.
  • the blank corrosion protection of the coatings according to the invention is often better at least by the time factor 20 or 30 than with comparable zinc-phosphated coatings.
  • composition of the invention is an unusually stable solution at an increased content of complexing agent even at very high levels of solids and active ingredients.
  • Aqueous solutions were used to coat hot dip galvanized sheets in the laboratory roll coater containing only an addition of zinc dihydrogen phosphate (60%) in the range of 40 to 100 g / L and a corresponding molar amount of orthophosphoric acid in deionized water.
  • the coatings showed in neutral salt spray test (NSS test) according to DIN EN ISO 9227 (blank corrosion test) after about 1 hour Corrosion phenomena of 1 to 5 area% and already after 8 hours full, thick, white layers of zinc corrosion products.
  • the condensate constant climate test according to DIN EN ISO 6270-2 (KK test) revealed white rust of up to 10 area% after 2 days. Such coatings are not usable in European industry for any use.
  • Aqueous compositions were mixed whose compositions are shown in Tables 1 as concentrates.
  • the dilution factor illustrates the dilution to the bath concentration used, that is from a concentrate to a bath, so that for example a concentrate used 200g and diluted with water to 1000g using dilution factor 5.
  • Aluminum was used as monoaluminum phosphate, chromium as Complexed chromium (II) fluoride and / or chromium (III) phosphonate, iron as ferric nitrate hydrate, manganese as manganese carbonate and / or manganese oxide, zinc as mono zinc phosphate and / or zinc oxide were added as silanes No.
  • TEOS N- (2-aminoethyl) -3-aminopropyltrimethoxysilane (AEAPS) and as No. 3) tetraethoxysilane (TEOS).
  • the complexing agents used as No. 1) were 1-hydroxyethane-1,1-diphosphonic acid (HEDP) and as No. 2) phytic acid.
  • Hexafluorotitanic acid, hexafluorozirconic acid or dihydroxo-bis (ammonium lactate) titanate were added as the titanium or zirconium compound.
  • the wax used was a wax emulsion based on oxidized polyethylene.
  • at least one glycol, in particular at least one polyethylene glycol is also possible to add at least one glycol, in particular at least one polyethylene glycol.
  • the adjustment of the pH was optionally carried out by means of aqueous ammonia solution. The range of pH values apply simultaneously to concentrates and bath concentrations. When diluting the concentrates to make bath solutions, care was taken to avoid precipitation. Concentrates and bath solutions were stored at room temperature for one to 24 hours before use.
  • the sheets were pre-cleaned with a cloth to largely remove adherent corrosion protection oil and to achieve an even distribution of the oil or other contaminants. Subsequently, the panels were spray-cleaned with a mildly alkaline, silicate-free powder cleaner until complete wettability with water was present. The duration for this was generally 20 to 30 s. This was followed by rinsing with city water in the dipping, rinsing with city water for 6 s by spraying and rinsing with demineralised water for 6 s. The majority of the adhered water was then removed from the sheets by squeezing between two rubber rolls. Subsequently, the sheets were blown dry with oil-free compressed air.
  • the dry sheets were contacted by means of a laboratory roll coater with the aqueous composition of about 25 ° C.
  • the pH of the compositions was determined with pH indicator paper.
  • a wet film of about 9 to 10 ⁇ m thickness was applied. By drying this wet film, a dry film of 0.2 to 0.6 microns thickness was produced.
  • the sheets treated in this way were dried at about 40 or 65 ° C. PMT. Subsequently, the edges of the coated sheets were taped with commercially available adhesive tape to eliminate edge effects during the corrosion test.
  • the coated sheets were then tested for their bare corrosion protection in the condensed water constant climatic test (KK test) according to DIN EN ISO 6270-2 and in the neutral salt spray test (NSS test) in accordance with DIN EN ISO 9227. The evaluation was done visually. The values given for the corrosion correspond to the percentage of the surface area of the total, corresponding to the chemical load (100%). In Galvalume ® -Blechen "black rust” and “white rust" were evaluated in total. The results of the corrosion tests illustrate the range of corrosion protection, using all measurement results including the measured values, which are to be regarded as outliers.
  • Comparative Examples VB 5 to VB 7 electrolytically galvanized sheets (ZE) were contacted with typical zinc-containing phosphating solutions after prior mild alkaline cleaning, rinsing with tap water and activation with titanium phosphate.
  • the phosphating was carried out in Comparative Examples VB 5 and VB 6 at temperatures in the range of room temperature to 40 ° C by spraying and rinsing (rinse method), in Comparative Example VB 7 at 55 to 60 ° C by rolling and drying (no-rinse -Method). The former were also oiled or rinsed.
  • the coatings produced according to the invention showed a coating weight in the range from 350 to 650 mg / m 2 overall coverage and a layer thickness approximately in the range from 0.2 to 0.6 ⁇ m. They were produced so thin and so fast that the substances in the coatings are not sufficiently crystalline to be determined by X-ray analysis. Scanning electron micrographs of these coatings essentially reveal the topography of the cleaned metallic substrate surface.
  • the applied coatings of the invention have not significantly topographically imaged under the scanning electron microscope.
  • the coatings are apparently homogeneous transparent layers. Depending on the substrate type and coating, they give the metallic surface a light matte finish, just as well as without a coating or with a stronger shine.
  • the coatings are usually without color cast.
  • compositions have in Comparative Example CE 1a and in Examples B 2 to B 6 each aluminum and zinc whose contents have been varied.
  • the KK test for 10 days on the associated coatings was flawless.
  • examples B 7 to B 13 in particular were varied PO 4 content, Ti content, pH, complexing agent type and silane type. At lower phosphate content, the corrosion protection may decrease. This may particularly affect the results of the KK test.
  • the complexing agent 1) behaved better than the complexing agent 2).
  • the silanes 1) and 2) behaved slightly better than the silane 3).
  • Examples B 14 and B 15 were as cations zinc and
  • Examples B 16 and B 17 compare the addition of a titanium compound with the addition of a zirconium compound. The addition of a titanium compound allows significantly higher corrosion protection on hot-dip galvanized surfaces. In Examples B 18 to B 21, various corrosion inhibitors were additionally used. The corrosion inhibitors improve the corrosion protection, with the corrosion inhibitor 4) acting somewhat less protective. The addition of tannin in Example B 22 brought no significant improvement. In Examples B 23 to B 25 and Comparative Example VB 26, the additions of cations were varied. The addition of chromium (III) improved the corrosion protection very clearly. The use of only iron cations was less successful for corrosion protection.
  • Example B 27 to B 32 Galvalume ® an excellent corrosion protection showed.
  • a silane additive is not necessary for Galvalume ® surfaces, but it is advantageous for high corrosion protection.
  • Example B 33 proves that even on Galfan ® surfaces good corrosion protection results are obtained.
  • Example B 34 and Comparative Example CE 35 for Alusi ® surfaces is important to ensure that the cation and phosphate content is not too low.
  • Examples B 36 to B 42 and in Comparative Examples VB43 and VB44 again hot-dip galvanized surfaces were coated.
  • Examples B 36 to B 41 was worked with or without silane and with varlierendem titanium compound content. The addition of silane or an increased titanium compound content resulted in better corrosion protection.
  • the complexing agent 1) usually behaves better than the complexing agent 2).
  • Example B 42 Exchanging titanium complex fluoride with a titanium chelate in Example B 42 resulted in excellent corrosion protection for a silane-free and fluoride-free composition.
  • Comparative Examples VB 43 and VB 44 only aluminum was used as cations. The associated coatings appeared a bit dull. The corrosion protection was good.
  • the blank corrosion protection of the examples according to the invention determined in the NSS test is usually better at least by the time factor 20 or 30 than with comparable zinc-phosphated coatings.
  • the main reason for this is assumed that the coating according to the invention is unusually closed and non-porous.

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Claims (14)

  1. Procédé de revêtement et de passivation de surfaces métalliques au moyen d'une composition aqueuse sous forme de solution ou de dispersion, caractérisé en ce que la composition contient
    - de 6 à 400 g/L d'au moins un phosphate, teneur calculée en PO4,
    - de 3 à 200 g/L d'au moins un composé de titane et/ou de zirconium,
    - de 1 à 200 g/L d'au moins un agent complexant, choisi dans l'ensemble des composés à base d'acide phosphonique, de phytine ou de tanin, étant entendu que la teneur en composés à base d'acide phosphonique est nulle ou vaut de 1 à 200 g/L et que la teneur en composés à base de phytine et/ou de tanin est nulle ou vaut de 0,05 à 30 g/L,
    - et de 3,5 à 100 g/L de cations d'aluminium, de chrome-III et/ou de zinc, et/ou d'au moins un composé contenant de l'aluminium, du chrome-III et/ou du zinc, teneur calculée en métaux,
    et en ce que l'on fait sécher un film humide de la composition aqueuse sur des rubans métalliques ou des tôles, sans rincer avec de l'eau le film humide ou le film séché.
  2. Procédé conforme à la revendication 1, caractérisé en ce que la composition contient en outre des cations de fer et/ou de manganèse et/ou au moins un composé contenant du fer et/ou du manganèse.
  3. Procédé conforme à la revendication 2, caractérisé en ce que la composition présente une teneur totale en cations d'aluminium, de chrome-III, de fer, de manganèse et/ou de zinc, et/ou en au moins un composé contenant de l'aluminium, du chrome-III, du fer, du manganèse et/ou du zinc, située dans l'intervalle allant de 3,5 à 100 g/L, teneur calculée en métaux.
  4. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition ne contient pour l'essentiel que des cations d'aluminium, de fer, de manganèse, de titane, de zinc et/ou de zirconium.
  5. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition présente une teneur totale en au moins un composé de titane et/ou de zirconium à base de fluorure complexe située dans l'intervalle allant de 1 à 200 g/L.
  6. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition présente une teneur en fluor libre Flibre située dans l'intervalle allant de 0,01 à 5 g/L, et/ou une teneur totale en fluor Ftotal située dans l'intervalle allant de 3 à 180 g/L.
  7. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition contient au moins un silane-sila-nol-siloxane-polysiloxane.
  8. Procédé conforme à la revendication 7, caractérisé en ce que la composition présente une teneur en au moins un silane-silanol-siloxane-polysiloxane située dans l'intervalle allant de 0,1 à 200 g/L, teneur calculée sur la base du silane ou polysiloxane du composé de départ respectif.
  9. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition contient au moins un adjuvant, comme par exemple un agent mouillant, un désémulsifiant, un émulsifiant, un agent de démoussage, un inhibiteur de corrosion et/ou une cire, dans chaque cas au nombre d'au moins un(e).
  10. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition présente un pH situé dans l'intervalle allant de 0 à 10.
  11. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la composition présente une valeur de l'indice d'acide libre (AL) située dans l'intervalle allant de 2 à 25 points, une valeur de l'indice d'acide total (AT) située dans l'intervalle allant de 20 à 45 points, et une valeur de l'indice d'acide total Fischer (ATF) située dans l'intervalle allant de 12 à 20 points.
  12. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que l'on traite avec la composition aqueuse, en tant que surfaces métalliques, des surfaces à base d'aluminium, de fer, de magnésium, de titane, de zinc et/ou d'étain, en particulier des pièces, des rubans et/ou des tôles.
  13. Revêtement préparé selon un procédé conforme à l'une des revendications 1 à 12 sur une surface métallique.
  14. Utilisation de composants métalliques, revêtus selon un procédé conforme à l'une des revendications 1 à 12, dans la construction de véhicules, en tant qu'éléments d'architecture dans la construction de bâtiments, ou pour la fabrication d'appareils et de machines comme par exemple des appareils ménagers.
EP09719612.5A 2008-03-11 2009-03-10 Procédé d enduction de surfaces métalliques avec un agent de passivation Active EP2255025B2 (fr)

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PL09719612T PL2255025T5 (pl) 2008-03-11 2009-03-10 Sposób powlekania powierzchni metalowych za pomocą środka do pasywacji

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DE102008000600A DE102008000600B4 (de) 2008-03-11 2008-03-11 Verfahren zur Beschichtung von metallischen Oberflächen mit einem Passivierungsmittel, das Passivierungsmittel, die hiermit erzeugte Beschichtung und ihre Verwendung
PCT/EP2009/052767 WO2009112480A1 (fr) 2008-03-11 2009-03-10 Procédé d’enduction de surfaces métalliques avec un agent de passivation, agent de passivation et son utilisation

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EP (1) EP2255025B2 (fr)
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DE (1) DE102008000600B4 (fr)
ES (1) ES2547119T5 (fr)
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Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008044143B4 (de) * 2008-11-27 2011-01-13 Atotech Deutschland Gmbh Wässrige Behandlungslösung und Verfahren zur Erzeugung von Konversionsschichten für zinkhaltige Oberflächen
CH702143A1 (de) * 2009-11-02 2011-05-13 Andre Egli Methode zur Beschichtung von Magnesium, Magnesium-Legierungen und weiteren Metallen mit Oberflächen-Oxiden.
US9039845B2 (en) 2009-11-04 2015-05-26 Bulk Chemicals, Inc. Trivalent chromium passivation and pretreatment composition and method for zinc-containing metals
EP2614175B1 (fr) * 2010-09-10 2018-01-03 Chemetall GmbH Procédé de revêtement de surfaces métalliques par un agent de revêtement contenant un polymère, agent de revêtement correspondant et son utilisation
DE102010047197A1 (de) 2010-09-30 2012-04-05 Daimler Ag Werkstück mit Kanten-Korrosionsschutzschicht und Verfahren zu dessen Herstellung
CN102816486B (zh) * 2011-06-10 2015-04-22 上海建冶科技工程股份有限公司 免除锈环保丙烯酸磷酸锌有机复合陶瓷防腐涂料及其制备方法
US20130115470A1 (en) * 2011-11-03 2013-05-09 Christian Schade Preparation for passivating metallic surfaces, comprising acid-functional polymers and ti or zr compounds
KR101554074B1 (ko) * 2012-11-30 2015-09-17 주식회사 엘지화학 롤
ES2656339T3 (es) 2012-12-11 2018-02-26 Thyssenkrupp Steel Europe Ag Agente acuoso y procedimiento de revestimiento para el tratamiento protector frente a la corrosión de sustratos metálicos
JP6216936B2 (ja) * 2013-01-24 2017-10-25 ユケン工業株式会社 反応型化成処理用酸性組成物および化成皮膜をその表面に備える部材の製造方法
DE102013215441A1 (de) * 2013-08-06 2015-02-12 Henkel Ag & Co. Kgaa Metallvorbehandlungszusammensetzungen umfassend Silane und Organophosphonsäuren
DE102013215440A1 (de) * 2013-08-06 2015-02-12 Henkel Ag & Co. Kgaa Metallvorbehandlung mit sauren wasserhaltigen Zusammensetzungen umfassend Silane
CN103497597B (zh) * 2013-09-23 2015-09-16 无锡阳工机械制造有限公司 一种钢板表面防腐涂布剂
CN103695892B (zh) * 2013-12-23 2016-03-02 奎克化学（中国）有限公司 用于镀锌材料的基于复合封闭技术的钝化液及其制备方法
US20150232671A1 (en) * 2014-02-20 2015-08-20 Ppg Industries Ohio, Inc. Pretreatment of magnesium substrates
WO2015124322A1 (fr) * 2014-02-20 2015-08-27 Tata Steel Ijmuiden B.V. Traitement d'activation de substrats d'acier revêtus
FR3021324B1 (fr) * 2014-05-23 2017-12-22 A Et A Mader Composition liante, procede de fabrication d'un revetement de protection sacrificielle contre la corrosion mettant en oeuvre ladite composition et support revetu d'un tel revetement
DE102014119472A1 (de) 2014-12-22 2016-06-23 Leibniz-Institut Für Neue Materialien Gemeinnützige Gmbh Verfahren zur Herstellung von anisotropen Zinkphosphat-Partikeln und Zink-Metall-Mischphosphatpartikeln und ihre Verwendung
CN104962892A (zh) * 2015-06-13 2015-10-07 梁胜光 一种用于铜带表面的钝化剂
US9915006B2 (en) 2015-07-10 2018-03-13 Yuken Industry Co., Ltd. Reactive-type chemical conversion treatment composition and production method of member with chemical conversion coated surface
CN106581778B (zh) * 2015-10-14 2020-07-21 先健科技(深圳)有限公司 可吸收铁基合金植入医疗器械及其制备方法
US10113070B2 (en) * 2015-11-04 2018-10-30 Ppg Industries Ohio, Inc. Pretreatment compositions and methods of treating a substrate
KR20180134330A (ko) * 2016-02-02 2018-12-18 시큐리티 매터스 엘티디. 금속 대상물의 인증
FR3047491B1 (fr) * 2016-02-09 2018-01-19 Safran Elaboration d'un traitement anti-corrosion par voie sol-gel
CN105779982B (zh) * 2016-05-17 2017-12-05 广东海洋大学 一种无铬金属表面转化液及转化膜制备方法
JP6870983B2 (ja) * 2016-12-27 2021-05-12 日本ペイント・サーフケミカルズ株式会社 亜鉛系メッキ鋼板用表面処理剤
HUE047403T2 (hu) * 2017-04-21 2020-04-28 Henkel Ag & Co Kgaa Lerakódásmentes foszfátbevonat-képzési módszer fémalkatrész sorozatokhoz
EP3392376A1 (fr) 2017-04-21 2018-10-24 Henkel AG & Co. KGaA Procédé formant des couches de phosphatate de zinc sur des composants métalliques en série
CN107815678A (zh) * 2017-10-23 2018-03-20 安徽屹翔滤材有限公司 一种不锈钢筛板表面钝化防腐处理方法
CN107937918A (zh) * 2017-11-18 2018-04-20 武汉钢铁有限公司 防锈剂及其制备方法和其对酸轧中间库冷硬钢卷的防锈应用
EP3569734A1 (fr) * 2018-05-18 2019-11-20 Henkel AG & Co. KGaA Composition de passivation à base de chrome trivalent
FI3663435T3 (fi) * 2018-12-05 2024-05-24 Henkel Ag & Co Kgaa Fosfori- ja fosfonihappojen seoksiin perustuva passivointikoostumus
CN109911955B (zh) * 2018-12-17 2022-08-23 熊映明 铝加工厂粉末喷涂铬化车间对废水中心零排放设计
CN110560344B (zh) * 2019-07-25 2022-02-22 广东省建筑科学研究院集团股份有限公司 一种与feve氟碳粉末涂料兼容的铝合金表面ats复合膜及其制备方法
WO2021139955A1 (fr) * 2020-01-06 2021-07-15 Henkel Ag & Co. Kgaa Composition de passivation appropriée pour des surfaces internes de réservoirs d'acier revêtus de zinc stockant des hydrocarbures
CN113881933B (zh) * 2021-08-20 2023-11-17 浙江万众新材料有限公司 一种无铬钝化液及其制备方法及使用方法
CN113943019A (zh) * 2021-10-18 2022-01-18 中南大学 一种从含铬、铁溶液中分离铬铁的方法
WO2023102284A1 (fr) * 2021-12-03 2023-06-08 Ppg Industries Ohio, Inc. Systèmes et procédés de traitement d'un substrat

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995004169A1 (fr) 1993-07-30 1995-02-09 Henkel Corporation Composition et procede de traitement des metaux
WO2000071626A1 (fr) 1999-05-20 2000-11-30 Henkel Kommanditgesellschaft Auf Aktien Agent anticorrosif depourvu de chrome et procede de protection contre la corrosion
US20030188807A1 (en) 2000-09-22 2003-10-09 Meagher Kevin K. Composition and process for treating metals
US20040009300A1 (en) 2000-10-11 2004-01-15 Toshiaki Shimakura Method for pretreating and subsequently coating metallic surfaces with paint-type coating prior to forming and use og sybstrates coated in this way

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4187127A (en) * 1978-12-07 1980-02-05 Nihon Parkerizing Co., Ltd. Surface processing solution and surface treatment of aluminum or aluminum alloy substrate
US4470853A (en) * 1983-10-03 1984-09-11 Coral Chemical Company Coating compositions and method for the treatment of metal surfaces
JP2879344B2 (ja) * 1989-04-07 1999-04-05 富山化学工業株式会社 ３―ホルミルアミノ―７―メチルスルホニルアミノ―６―フェノキシ―４ｈ―１―ベンゾピラン―４―オンまたはその塩を含有する抗炎症製剤
US5449415A (en) * 1993-07-30 1995-09-12 Henkel Corporation Composition and process for treating metals
US5380374A (en) * 1993-10-15 1995-01-10 Circle-Prosco, Inc. Conversion coatings for metal surfaces
CA2234146C (fr) * 1995-10-10 2003-07-08 Courtaulds Aerospace, Inc. Inhibiteurs de corrosion exempts de chromate pour alliages d'aluminium
DE19754108A1 (de) * 1997-12-05 1999-06-10 Henkel Kgaa Chromfreies Korrosionsschutzmittel und Korrosionsschutzverfahren
AU6298400A (en) * 1999-07-26 2001-02-13 Chemetall Plc Metal surface treatment
DE10010355A1 (de) * 2000-03-07 2001-09-13 Chemetall Gmbh Verfahren zum Aufbringen eines Phosphatüberzuges und Verwendung der derart phosphatierten Metallteile
US6530999B2 (en) * 2000-10-10 2003-03-11 Henkel Corporation Phosphate conversion coating
MY117334A (en) * 2000-11-10 2004-06-30 Nisshin Steel Co Ltd Chemically processed steel sheet improved in corrosion resistance
JP2004521187A (ja) * 2001-02-16 2004-07-15 ヘンケル・コマンディットゲゼルシャフト・アウフ・アクチエン 多金属物品を処理する方法
JP2003193255A (ja) * 2001-12-26 2003-07-09 Kansai Paint Co Ltd 金属材料用表面処理組成物
AU2003250917A1 (en) * 2002-07-10 2004-02-02 Chemetall Gmbh Method for coating metallic surfaces
US6881279B2 (en) * 2002-12-11 2005-04-19 Henkel Corporation High performance non-chrome pretreatment for can-end stock aluminum
CA2454208A1 (fr) * 2002-12-24 2004-06-24 Nippon Paint Co., Ltd. Agent de revetement par conversion chimique et metal a surface traitee
DE10323305B4 (de) * 2003-05-23 2006-03-30 Chemetall Gmbh Verfahren zur Beschichtung von metallischen Oberflächen mit einer Wasserstoffperoxid enthaltenden Phosphatierungslösung, Phosphatierlösung und Verwendung der behandelten Gegenstände
DE102005015573B4 (de) * 2005-04-04 2014-01-23 Chemetall Gmbh Verfahren zur Beschichtung von metallischen Oberflächen mit einer wässerigen Silan/Silanol/Siloxan/Polysiloxan enthaltenden Zusammensetzung, diese wässerige Zusammensetzung und Verwendung der nach dem Verfahren beschichteten Substrate
US8101014B2 (en) * 2004-11-10 2012-01-24 Chemetall Gmbh Process for coating metallic surfaces with a multicomponent aqueous composition
EP1815044B1 (fr) * 2004-11-10 2019-06-19 Chemetall GmbH Procede pour recouvrir des surfaces metalliques au moyen d'une composition aqueuse comprenant les composés silane/silanol/siloxane/polysiloxane et la dite composition
US20060099332A1 (en) * 2004-11-10 2006-05-11 Mats Eriksson Process for producing a repair coating on a coated metallic surface
DE102005023023B4 (de) * 2005-05-19 2017-02-09 Chemetall Gmbh Verfahren zur Vorbereitung von metallischen Werkstücken zum Kaltumformen, mit dem Verfahren beschichtete Werkstücke und ihre Verwendung
US7947333B2 (en) * 2006-03-31 2011-05-24 Chemetall Gmbh Method for coating of metallic coil or sheets for producing hollow articles
DE102006052919A1 (de) * 2006-11-08 2008-05-15 Henkel Kgaa Zr-/Ti-haltige Phosphatierlösung zur Passivierung von Metallverbundoberflächen

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995004169A1 (fr) 1993-07-30 1995-02-09 Henkel Corporation Composition et procede de traitement des metaux
WO2000071626A1 (fr) 1999-05-20 2000-11-30 Henkel Kommanditgesellschaft Auf Aktien Agent anticorrosif depourvu de chrome et procede de protection contre la corrosion
US20030188807A1 (en) 2000-09-22 2003-10-09 Meagher Kevin K. Composition and process for treating metals
US20040009300A1 (en) 2000-10-11 2004-01-15 Toshiaki Shimakura Method for pretreating and subsequently coating metallic surfaces with paint-type coating prior to forming and use og sybstrates coated in this way

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CN102027157B (zh) 2013-07-31
US20170314137A1 (en) 2017-11-02
DE102008000600B4 (de) 2010-05-12
MX2010009941A (es) 2010-11-25
ZA201007246B (en) 2012-01-25
JP5562261B2 (ja) 2014-07-30
CN102027157A (zh) 2011-04-20
WO2009112480A1 (fr) 2009-09-17
EP2255025B2 (fr) 2018-07-18
CA2718242A1 (fr) 2009-09-17
AU2009224757B2 (en) 2013-08-29
PL2255025T3 (pl) 2015-11-30
ES2547119T5 (es) 2018-11-26
CA2718242C (fr) 2017-05-16
AU2009224757A1 (en) 2009-09-17
EP2255025A1 (fr) 2010-12-01
PL2255025T5 (pl) 2018-12-31
ES2547119T3 (es) 2015-10-01
US20110008645A1 (en) 2011-01-13
JP2011517727A (ja) 2011-06-16

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